WO1988009354A1 - Plastiques degradables - Google Patents

Plastiques degradables Download PDF

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Publication number
WO1988009354A1
WO1988009354A1 PCT/GB1988/000386 GB8800386W WO8809354A1 WO 1988009354 A1 WO1988009354 A1 WO 1988009354A1 GB 8800386 W GB8800386 W GB 8800386W WO 8809354 A1 WO8809354 A1 WO 8809354A1
Authority
WO
WIPO (PCT)
Prior art keywords
polymer
polymer composition
oxidant
natural
unsaturated compound
Prior art date
Application number
PCT/GB1988/000386
Other languages
English (en)
Inventor
Gerald Joseph Louis Griffin
Original Assignee
Epron Industries Limited
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Epron Industries Limited filed Critical Epron Industries Limited
Priority to EP88904254A priority Critical patent/EP0363383B1/fr
Priority to KR1019890700106A priority patent/KR970004917B1/ko
Priority to DE3854431T priority patent/DE3854431T2/de
Publication of WO1988009354A1 publication Critical patent/WO1988009354A1/fr
Priority to NO890212A priority patent/NO890212D0/no
Priority to FI895517A priority patent/FI98732C/fi
Priority to DK198905823A priority patent/DK173143B1/da

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00—Use of organic ingredients
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00—Use of organic ingredients
    • C08K5/0008—Organic ingredients according to more than one of the "one dot" groups of C08K5/01 - C08K5/59
    • C08K5/0033—Additives activating the degradation of the macromolecular compound
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L57/00—Compositions of unspecified polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds

Definitions

  • This invention relates to degradable synthetic polymer compositions.
  • packaging items such as bags and containers are destined, after a relatively short functional life, to arrive as a significant component of urban garbage or, to a much lesser extent, in the form of litter-
  • packaging items are being manu ⁇ factured from plastics, that is to say from synthetic polymer compositions, which, whilst being cheap and having the physical properties which make them highly suitable for such packaging purposes, have the dis ⁇ advantage, as components of waste or garbage, of being highly resistant to destruction by the chemical and physical actions to which they are subject in the natural environment and thereby such components constitute a mounting nuisance-
  • the first, chemical, stage of this degradation process can follow different mechanisms which can be broadly classified under two headings the first being photochemical oxidative chain scission, and the second chemical catalytic oxidative chain scission.
  • the present invention to provide a synthetic polymer capable of undergoing degradation under the conditions to which items made therefrom are subject when they form a component of garbage disposed of by the landfill or composting route of garbage disposal.
  • a degradable polymer composition which incor ⁇ porates a normally stable chemically saturated polymer, a - i t-
  • a degradable polymer composition which comprises a blend of a normally stable chemically saturated polymer, a less stable chemically unsaturated compound in the form of a polymer or copolymer, an antioxidant active over a limited period and a latent pro-oxidant, the presence together of the anti-oxidant and the pro-oxidant giving rise to a period of induction before a sharp loss of physical strength occurs, whereby the period of induction can be exploited as the effective working life of the polymer composition.
  • the stable polymer is preferably a polyethylene such as low-density polyethylene, linear low-density polyethylene or high density polyethylene. Alternat ⁇ ively, the stable polymer may be polypropylene or polystyrene.
  • the associated unsaturated compound may be an elastomer of the type made by the polymerisation of 1:4 dienes, or the copolymerisation of such 1:4 dienes with ethenoid comonomers.
  • compositions embodying the invention form a class of polymer formulations, the lifetime of which is divided into two zones. This is achieved by exploiting the phenomenon of the induction period which can be noted when an oxidation sensitive material is protected by selected types of protective chemical additives generally called antioxidants.
  • antioxidants are a normal Ingredient of most packaging polymer formulations, being required initially to protect the polymer during the extreme thermal stresses of compound ⁇ ing and conversion processing.
  • compositions in accordance with the invention can be produced which, whilst being adequately stable for the duration of the essentially anaerobic conversion processing in enclosed machinery such as extruders, will subsequently reach the point at which the anti-oxidant is expended and the system enters into its second time zone during which oxidation takes place.
  • This oxidation ideally commences after a passage of time which, at normal room tem ⁇ perature, safely exceeds the normal functional life of such products.
  • compositions embodying the invention substances capable of autoxidation because such substances are more readily initiated into the oxidation process by virtue of their unsaturation and, once initiated, the chemical processes can involve the more resistant saturated molecular structures of the common packaging thermoplastics such as the poly- olefines.
  • the unsaturated poly ⁇ meric component of a composition embodying the invention natural rubber or particular styrene-butadiene elasto ⁇ mers which not only provide adequate levels of autoxidis- able unsaturation but also greatly Improve some of the physical properties of the products especially their impact strength.
  • Transition metal salts are preferred as pro-oxidants for these degradable compositions and it has been found that, provided that the anti-oxidant and pro- oxidant types and ratios are correctly selected and adhered to, then transition metal compounds capable of the oxygen transfer chemistry can be incorporated into polymer compositions jointly with anti-oxidant ingred ⁇ ients in the compounding operation.
  • transition metal salts used in preferred embodiments are salts formed by combining transition _ ? _
  • metals such as cobalt, manganese and copper with organic acids of sufficiently high molecular weight to give salts soluble in the host polymer blends used.
  • transition metal as used herein means an element having greater than 8 and less than 18 electrons in the outer group of the ion. Transition metals are thus usually capable of electron transitions between their outer shells and the variable valency states resulting render them capable of inducing oxidation reactions. In practice, those transition elements which are highly toxic, radioactive, are extremely rare and costly are not normally encountered in industrial use as oxidation catalysts. Typical transition metals whose salts and complexes do feature in such applications and could be considered for use in carrying out the present invention are Ce, Zn, Cu, Ag, Ni , Co, Fe, Mn, Cr, and V.
  • salts typically display an adequate level of solubility in polymer melts, typically stearates, oleates, behenates, yristates, erucates, linoleates, or naphthenates, or complexes such as ace- tonylacetates, 8-hydroxyquinolinates, metalamine salt complexes and the like.
  • the trans ⁇ ition metal salts may be used in quantities such as to provide from 0.001$ to 1 % by weight of the metal in the composition, depending upon the desired oxidation rate.
  • the anti-oxidant used is generally that incorporated as a matter of course in the manufacture of the respective chemically saturated polymer.
  • commercially supplied polyolefine mater ⁇ ials are normally sold containing a variety of well established anti-oxidants and any of these antioxidants can be used in the compositions of this invention.
  • Typical of such anti-oxidants is the ICI product Topanol (4-methyl-1 , 6-di(2-hydroxy-3-tertbutyl-5-methylbenzyl)- phenol used for stabilising most low-density poly ⁇ ethylene (LDPE) materials.
  • LDPE low-density poly ⁇ ethylene
  • the proportion of the unsaturated polymer or copolymer in a composition embodying the invention may be in the range 0.5$ to 50$ by weight of the composition, preferably between 2$ and 15$ in order to balance the factors of cost, adequate oxidation effect, and adequate restoration of strength loss due to the presence of starch where used.
  • the starch content may be from 0.5 to 50$ by weight of the composition, although mechanical strength of the composition at the higher end of this range tends to be low.
  • the starch content is from 2$ to 15$ by weight of the co.mposition.
  • compositions embodying the invention when items formed from compositions embodying the invention are buried or composted with other garbage, degradation commences early in the second time zone, with oxidation following depletion of the antioxidant. Also commencing early in the second time zone is the interaction between the micro-organisms occurring profusely in the garbage environment and the partly oxidised polymers. It has been observed that the inclusion of particulate organic fillers such as starch into synthetic polymer formulations can have an acceler ⁇ ating effect on the biological breakdown of those polymers which are themselves intrinsically sensitive to direct enzyme chain scission.
  • compositions embodying the invention are dis ⁇ closed, by way of illustration, in the examples in the following description.
  • FIGURE 1 is a graph illustrating variation of ultimate tensile strength (UTS) with time for a first composition embodying the invention
  • FIGURE 2 is a graph illustrating variation of percentage strength retention with time for a second composition embodying the invention and a control material not embodying the invention.
  • FIGURE 3 is a graph illustrating variation of break energy for standardised samples, with incubation time of the material, for two different compositions embodying the invention and illustrating the effect of varying the percentage of pro-oxidant, and
  • FIGURE 4 is a graph showing weight change, as an indication of oxidation, over a period of time, and illustrating the effect of the incorporation of natural rubber, as the unsaturated polymer, in a composition embodying the invention, as contrasted with a material which is of substantially the same composition apart from the omission of rubber.
  • Polyethylene of melt flow index 2 and density 0.916 which would have contained a normal complement of heat stabiliser, was hot compounded on a two-roll mill at 150° Centigrade with its own weight of maize starch which had previously been oven dried to about 1$ moisture content. The hide stripped from the mill was cooled and cut into granules to provide a starch masterbatch. Further polyethylene of melt flow index 2 and density 0.916 was compounded on the mill with its own weight of a granular block copolymer of styrene and butadiene con ⁇ taining 40$ of styrene and reported by its manufacturers, Phillips Petroleum, to have a molecular weight of 130,000.
  • the hide stripped from the mill was again cooled and cut into granules to provide a synthetic rubber masterbatch.
  • a cold mix of granules was prepared containing 10$ of dry starch and 5$ of the synthetic rubber.
  • a quantity of a solution of cobalt naphthenate in white spirit was added calculated to provide a cobalt concen ⁇ tration of 0.01$ in the total mix by virtue of the cobalt content of the white spirit solution being 10$.
  • a pilot plant for film blowing was set up working with the same polyethylene grade as was used for the blend of master ⁇ batches so that the film thickness was close to 50 micrometers and, when the operating conditions were stable, the feed hopper was emptied and the cold blend of masterbatches and polyethylene was introduced into the hopper.
  • the operation of cne machine continued undis ⁇ turbed by the change of material and it was easy, knowing the characteristics of the particular machine, to collect film samples which had essentially the same composition as the feed blend material. Samples were cut from this film for test purposes some of which were tested for tensile properties immediately and others suspended in an incubator maintained at 70° Centigrade with internal forced air circulation so that samples could be withdrawn every 24 hours for testing.
  • test temperature was chosen as representative of typical thermal conditions in garbage composting. Standard shape dumb bell samples were punched from the samples and they were tested essentially in accord with ASTM D.882-64T. It was very obvious that the tensile behaviour of the incubated material changed very little for about one week at the end of which time its ultimate tensile strength collapsed to a level so low that it could not be measured in the customary equipment. At the end of a further week the samples could not be picked up in the fingers without crumbling into fragments.
  • a roll of 50 micron thick low density polyethylene film was prepared exactly as described in Example I using the same formulation. From the roll rectangular sample pieces were cut measuring about 8cms by 20 cms in such a manner as to ensure that the extrusion direction of the film coincided in every case with the longer dimension of the test pieces thus ensuring that the subsequent strength measurements were strictly comparable in terms of possible extrusion orientation effects. In order to expose these film samples to comparable soil burial conditions they were all interred in the same plot of earth.
  • This plot was created by clearing a mature loam garden bed in the County of Surrey, U.K., of the previous year's growth, sieving the soil to a depth of about 20 cms through a inch riddle to remove large stones, raking the surface smooth to avoid the local collection of rainwater, and providing a horizontal wire mesh screen held clear of the surface by a light wooden frame to prevent digging or burrowing by cats, dogs, or rabbits.
  • the plastic film samples were buried individually in the test plot with each sample set on edge to ensure free drainage of water and to ensure all-round contact with the earth. The top edge of each sample was about 5 cms below the surface of the earth.
  • Control samples of LDPE film extrusion blown at the same thickness and from the same base polymer but without the starch, elastomer and prodegradant (pro-oxidant and starch) additives were buried at the same time and in the same manner. All the test samples were buried on the same day in the month of May and groups of samples were removed from the plot at intervals as required for testing. The disinterred samples were washed free of adhering soil particles and dried by exposing them in the test room environment at about 50$ relative humidity after blotting them free from surface moisture.
  • Cut samples from these two films measuring about 8cms by 20cms were suspended freely in an air circulated incubator maintained at an air temperature of 70° Centigrade plus or minus 1° Centigrade. Samples of both types of film were removed at convenient intervals, dumb ⁇ bell samples punched, and their tensile properties measured following the procedures of ASTM D882-64T. The load/elongation curves were recorded using an XY recorder linked to the analogue voltage outputs of the tensile testing machine and the areas of these curves measured using an image analysing device.
  • the technique of plotting breaking energy against time of exposure to test conditions has the advantage that it takes into account both the loss in tensile strength and the reduction of elongation at break which are commonly observed consequences of the oxidative degradation processes.
  • the pro-oxidant such as a transition metal salt
  • the pro-oxidant may be omitted from the polymer composition, and the presence of iron salts in the soil, or in the other garbage with which packaging or the like made from the polymer composition is buried or composted may be relied upon to promote oxidation of the unsaturated polymer or co ⁇ polymer in the composition blend whereby degradation may be initiated by the act of burying or composting the garbage.
  • a composition embodying the invention may be made into a degradable product comprising a thin film or sheet adapted for the manufacture of bags and wrappings, the thin film or sheet having been formed by extrusion, extrusion blowing, film casting or calendering the polymer composition.
  • a composition embodying the invention may alternatively be formed into three- dimensional objects such as containers or vessels, or disposable utility items, by injection moulding, blow moulding, compression moulding, thermoforming or rotational casting of the polymer composition.

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Biological Depolymerization Polymers (AREA)
  • Treatments Of Macromolecular Shaped Articles (AREA)
  • Processes Of Treating Macromolecular Substances (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Polymerisation Methods In General (AREA)
  • Materials For Medical Uses (AREA)
  • Macromonomer-Based Addition Polymer (AREA)

Abstract

La composition polymère dégradable décrite comprend un mélange constitué par un polymère chimiquement saturé et normalement stable, tel que du polyéthylène, par un polymère ou un copolymère chimiquement non saturé et moins stable, tel qu'un copolymère bloc de styrène-butadiène, ou par du caoutchouc naturel, par un agent anti-oxydant actif pendant une période limitée et par un pro-oxydant latent, tel qu'un sel organique d'un métal de transition, tel que du naphténate de cobalt. La présence conjointe de l'anti-oxydant et du pro-oxydant permet d'obtenir une période d'induction avant que ne se produise une brusque perte de la résistance physique, cette période d'induction pouvant être mise à profit comme la durée de vie utile effective de la composition polymère. La composition polymère comprend également de préférence des particules de charge constituées par un matériau directement bio-sensible tel que de l'amidon naturel, un dérivé d'amidon naturel, une protéine naturelle ou un produit cellulosique naturel ou encore un sucre en poudre dont le point de fusion est supérieur à la température de traitement de la composition polymère hôte. Ainsi, le fractionnement biologique, qui se produit dans des environnements naturels ou dans les lieux spécialement bio-actifs qui avoisinent les sites de compostage des déchets urbains et dont sont l'objet les fragments moléculaires créés par le début de scission par oxydation des chaînes moléculaires du polymère chimiquement saturé, est accéléré grâce à la présence de ces particules de charge.
PCT/GB1988/000386 1987-05-21 1988-05-16 Plastiques degradables WO1988009354A1 (fr)

Priority Applications (6)

Application Number Priority Date Filing Date Title
EP88904254A EP0363383B1 (fr) 1987-05-21 1988-05-16 Plastiques degradables
KR1019890700106A KR970004917B1 (ko) 1987-05-21 1988-05-16 분해가능한 플라스틱
DE3854431T DE3854431T2 (de) 1987-05-21 1988-05-16 Degradierbare kunststoffe.
NO890212A NO890212D0 (no) 1987-05-21 1989-01-18 Nedbrytbart plastmateriale.
FI895517A FI98732C (fi) 1987-05-21 1989-11-20 Biologisesti hajoavia polymeerikoostumuksia, jotka sisältävät tyydyttynyttä polymeeria ja tyydyttymätöntä polymeeriyhdistettä
DK198905823A DK173143B1 (da) 1987-05-21 1989-11-20 Nedbrydeligt polymermateriale samt nedbrydeligt produkt fremstillet deraf

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB8712009 1987-05-21
GB878712009A GB8712009D0 (en) 1987-05-21 1987-05-21 Degradable plastics

Publications (1)

Publication Number Publication Date
WO1988009354A1 true WO1988009354A1 (fr) 1988-12-01

Family

ID=10617692

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/GB1988/000386 WO1988009354A1 (fr) 1987-05-21 1988-05-16 Plastiques degradables

Country Status (12)

Country Link
US (1) US4983651A (fr)
EP (1) EP0363383B1 (fr)
JP (1) JPH02504037A (fr)
KR (1) KR970004917B1 (fr)
AT (1) ATE127497T1 (fr)
AU (1) AU626260B2 (fr)
CA (1) CA1335005C (fr)
DE (1) DE3854431T2 (fr)
FI (1) FI98732C (fr)
GB (1) GB8712009D0 (fr)
IL (1) IL86522A (fr)
WO (1) WO1988009354A1 (fr)

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US4985024A (en) * 1989-12-01 1991-01-15 Minnesota Mining And Manufacturing Company Disposable diaper having fastening means that are degradable
WO1991005982A1 (fr) * 1989-10-23 1991-05-02 The Kent Cartridge Manufacturing Company Limited Ameliorations apportees a des cartouches a plombs
WO1991006601A1 (fr) * 1989-11-02 1991-05-16 Allied-Signal Inc. Matieres polymeres biodegradables et articles fabriques a partir de celles-ci
US5070122A (en) * 1989-06-15 1991-12-03 Eastman Kodak Company Environmentally degradable polymer blends
GB2207439B (en) * 1987-07-27 1992-02-12 Metal Box Plc Improvements in and relating to packaging
US5112424A (en) * 1989-09-01 1992-05-12 Eastman Kodak Company Low temperature multi-layer extrusion coating process
US5111933A (en) * 1991-04-16 1992-05-12 Mobil Oil Corporation Kit providing thermally degradable compost bag
EP0546530A2 (fr) * 1991-12-11 1993-06-16 Kimberly-Clark Corporation Composition élastomère apte à l'extrusion à dégradation contrôlée
WO1993011941A2 (fr) * 1991-12-12 1993-06-24 Minnesota Mining And Manufacturing Company Structures multicouches degradables_____________________________
US5258422A (en) * 1992-05-05 1993-11-02 Tredegar Industries, Inc. Compostable thermoplastic compositions
WO1994025657A1 (fr) * 1993-05-05 1994-11-10 Kimberly-Clark Corporation Films et tissus non tisses stables a la conservation
EP0678111A1 (fr) * 1992-12-16 1995-10-25 Ecostar International L.P. Composes polymeres synthetiques degradables
GB2290741A (en) * 1994-06-28 1996-01-10 Frank Huang Disposable receptacle and method of forming the same
EP0775724A1 (fr) 1995-11-27 1997-05-28 Societe Nationale Des Poudres Et Explosifs Compositions entièrement biodégradables utiles pour fabriquer des cartouches de chasse et de tir
US6159404A (en) * 1989-06-15 2000-12-12 Eastman Chemical Company Low temperature, high speed extrusion coating process and polyethylene compositions useful therefor containing a thermally sensitive additive
US6482872B2 (en) 1999-04-01 2002-11-19 Programmable Materials, Inc. Process for manufacturing a biodegradable polymeric composition
WO2015033081A1 (fr) 2013-09-06 2015-03-12 J.C. Shotwell & Sons Munition de chasse comprenant une composition thermoplastique biodégradable
US9668913B2 (en) 2010-03-31 2017-06-06 Kobayashi Pharmaceutical Co., Ltd. Biodegradable disposable hand warmer
WO2018124122A1 (fr) 2016-12-28 2018-07-05 ユニ・チャーム株式会社 Article absorbant
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FI91643C (fi) * 1989-10-05 1994-07-25 Biostor Oy Biologisesti hajoava kalvo ja menetelmä sellaisen valmistamiseksi
CA2040993C (fr) * 1990-04-25 2001-08-07 Yoshiaki Inoue Composition qui absorbe l'oxygene et methode de conservation d'un article grace a cette composition
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HU216133B (hu) * 1991-06-26 1999-04-28 Procter And Gamble Co. Biológiailag lebontható, folyadékot át nem eresztő fólia
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US7402618B2 (en) * 2000-11-23 2008-07-22 Hao Xu Biodegradable composition for the preparation of tableware, drink container, mulching film and package and method for preparing the same
US20020183418A1 (en) * 2001-02-02 2002-12-05 Oren Rosen Design and synthesis of instant-degradable plastics
KR20020029050A (ko) * 2002-03-29 2002-04-17 주식회사 나선하이테크 분해성 수지 및 그 제조방법
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US20040259974A1 (en) * 2003-06-18 2004-12-23 Gerald Scott Biodegradable polymer compositions with controlled lifetimes
US20090062413A1 (en) * 2003-10-24 2009-03-05 Crane Building Products Llc Composition of fillers with plastics for producing superior building materials
US20070227087A1 (en) * 2003-10-24 2007-10-04 Crane Plastics Company Llc Method of manufacturing simulated stone, brick, and masonry panels and wall structures
US20050087908A1 (en) * 2003-10-24 2005-04-28 Moe Nasr Simulated stone and masonry and brick textured siding panels
US7052628B2 (en) * 2003-11-19 2006-05-30 Chevron Phillips Chemical Company, Lp Transition metal carboxylates as catalysts for oxygen scavenging
US10400105B2 (en) 2015-06-19 2019-09-03 The Research Foundation For The State University Of New York Extruded starch-lignin foams

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US9668913B2 (en) 2010-03-31 2017-06-06 Kobayashi Pharmaceutical Co., Ltd. Biodegradable disposable hand warmer
WO2015033081A1 (fr) 2013-09-06 2015-03-12 J.C. Shotwell & Sons Munition de chasse comprenant une composition thermoplastique biodégradable
WO2018124122A1 (fr) 2016-12-28 2018-07-05 ユニ・チャーム株式会社 Article absorbant
US11433157B2 (en) 2016-12-28 2022-09-06 Unicharm Corporation Absorbent article

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EP0363383A1 (fr) 1990-04-18
CA1335005C (fr) 1995-03-28
IL86522A (en) 1992-07-15
FI895517A0 (fi) 1989-11-20
GB8712009D0 (en) 1987-06-24
EP0363383B1 (fr) 1995-09-06
JPH02504037A (ja) 1990-11-22
AU1716188A (en) 1988-12-21
DE3854431T2 (de) 1996-04-04
FI98732C (fi) 1997-08-11
DE3854431D1 (de) 1995-10-12
KR890701673A (ko) 1989-12-21
US4983651A (en) 1991-01-08
KR970004917B1 (ko) 1997-04-08
AU626260B2 (en) 1992-07-30
ATE127497T1 (de) 1995-09-15
FI98732B (fi) 1997-04-30

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